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EP3149111B1 - Méthode de traitement de déchets polymères - Google Patents

Méthode de traitement de déchets polymères Download PDF

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Publication number
EP3149111B1
EP3149111B1 EP15750623.9A EP15750623A EP3149111B1 EP 3149111 B1 EP3149111 B1 EP 3149111B1 EP 15750623 A EP15750623 A EP 15750623A EP 3149111 B1 EP3149111 B1 EP 3149111B1
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EP
European Patent Office
Prior art keywords
processing container
gate
cooling chamber
waste
cooling
Prior art date
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EP15750623.9A
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German (de)
English (en)
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EP3149111A1 (fr
Inventor
Hilmar Hubbes
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Individual
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Individual
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Priority to PL15750623T priority Critical patent/PL3149111T3/pl
Publication of EP3149111A1 publication Critical patent/EP3149111A1/fr
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Classifications

    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B53/00—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form
    • C10B53/07—Destructive distillation, specially adapted for particular solid raw materials or solid raw materials in special form of solid raw materials consisting of synthetic polymeric materials, e.g. tyres
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B09—DISPOSAL OF SOLID WASTE; RECLAMATION OF CONTAMINATED SOIL
    • B09B—DISPOSAL OF SOLID WASTE NOT OTHERWISE PROVIDED FOR
    • B09B3/00—Destroying solid waste or transforming solid waste into something useful or harmless
    • B09B3/40—Destroying solid waste or transforming solid waste into something useful or harmless involving thermal treatment, e.g. evaporation
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/02—Separating plastics from other materials
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
    • C10B47/02—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with stationary charge
    • C10B47/06—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with stationary charge in retorts
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10B—DESTRUCTIVE DISTILLATION OF CARBONACEOUS MATERIALS FOR PRODUCTION OF GAS, COKE, TAR, OR SIMILAR MATERIALS
    • C10B47/00—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion
    • C10B47/18—Destructive distillation of solid carbonaceous materials with indirect heating, e.g. by external combustion with moving charge
    • C—CHEMISTRY; METALLURGY
    • C10—PETROLEUM, GAS OR COKE INDUSTRIES; TECHNICAL GASES CONTAINING CARBON MONOXIDE; FUELS; LUBRICANTS; PEAT
    • C10G—CRACKING HYDROCARBON OILS; PRODUCTION OF LIQUID HYDROCARBON MIXTURES, e.g. BY DESTRUCTIVE HYDROGENATION, OLIGOMERISATION, POLYMERISATION; RECOVERY OF HYDROCARBON OILS FROM OIL-SHALE, OIL-SAND, OR GASES; REFINING MIXTURES MAINLY CONSISTING OF HYDROCARBONS; REFORMING OF NAPHTHA; MINERAL WAXES
    • C10G1/00—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal
    • C10G1/10—Production of liquid hydrocarbon mixtures from oil-shale, oil-sand, or non-melting solid carbonaceous or similar materials, e.g. wood, coal from rubber or rubber waste
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04—Disintegrating plastics, e.g. by milling
    • B29B17/0412—Disintegrating plastics, e.g. by milling to large particles, e.g. beads, granules, flakes, slices
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29B—PREPARATION OR PRETREATMENT OF THE MATERIAL TO BE SHAPED; MAKING GRANULES OR PREFORMS; RECOVERY OF PLASTICS OR OTHER CONSTITUENTS OF WASTE MATERIAL CONTAINING PLASTICS
    • B29B17/00—Recovery of plastics or other constituents of waste material containing plastics
    • B29B17/04—Disintegrating plastics, e.g. by milling
    • B29B2017/0424—Specific disintegrating techniques; devices therefor
    • B29B2017/0496—Pyrolysing the materials
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29K—INDEXING SCHEME ASSOCIATED WITH SUBCLASSES B29B, B29C OR B29D, RELATING TO MOULDING MATERIALS OR TO MATERIALS FOR MOULDS, REINFORCEMENTS, FILLERS OR PREFORMED PARTS, e.g. INSERTS
    • B29K2105/00—Condition, form or state of moulded material or of the material to be shaped
    • B29K2105/26—Scrap or recycled material
    • B—PERFORMING OPERATIONS; TRANSPORTING
    • B29—WORKING OF PLASTICS; WORKING OF SUBSTANCES IN A PLASTIC STATE IN GENERAL
    • B29L—INDEXING SCHEME ASSOCIATED WITH SUBCLASS B29C, RELATING TO PARTICULAR ARTICLES
    • B29L2030/00—Pneumatic or solid tyres or parts thereof
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/10—Process efficiency
    • Y02P20/129—Energy recovery, e.g. by cogeneration, H2recovery or pressure recovery turbines
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02P—CLIMATE CHANGE MITIGATION TECHNOLOGIES IN THE PRODUCTION OR PROCESSING OF GOODS
    • Y02P20/00—Technologies relating to chemical industry
    • Y02P20/141—Feedstock
    • Y02P20/143—Feedstock the feedstock being recycled material, e.g. plastics
    • Y—GENERAL TAGGING OF NEW TECHNOLOGICAL DEVELOPMENTS; GENERAL TAGGING OF CROSS-SECTIONAL TECHNOLOGIES SPANNING OVER SEVERAL SECTIONS OF THE IPC; TECHNICAL SUBJECTS COVERED BY FORMER USPC CROSS-REFERENCE ART COLLECTIONS [XRACs] AND DIGESTS
    • Y02—TECHNOLOGIES OR APPLICATIONS FOR MITIGATION OR ADAPTATION AGAINST CLIMATE CHANGE
    • Y02W—CLIMATE CHANGE MITIGATION TECHNOLOGIES RELATED TO WASTEWATER TREATMENT OR WASTE MANAGEMENT
    • Y02W30/00—Technologies for solid waste management
    • Y02W30/50—Reuse, recycling or recovery technologies
    • Y02W30/62—Plastics recycling; Rubber recycling

Definitions

  • the invention relates to a method of processing polymeric and / or organic waste, in particular rubber waste and bamboo chips.
  • Comparable treatment processes are also known for organic waste. So explains the DE 10 2005 038 827 A1 a pyrolysis process for converting bamboo waste into artificial coal. This is followed by crushing and re-binding the Coal with a binder. After reheating and carbonizing the coal, it can be used for adsorption purposes.
  • the DE 103 48 987 A1 discloses a two-stage thermal treatment. After pretreatment in a preheating chamber heated by the exhaust gases from a pyrolysis furnace, a reaction container is transferred to the pyrolysis furnace and closes it off with a specially designed reaction container cover. On the one hand, this increases the cost of producing such a reaction container and is particularly disadvantageous in terms of energy, since the pyrolysis furnace remains open from the removal of a process container until the subsequent use of a subsequent process container. The separation of the gas generated during pyrolysis into a condensed pyrolysis oil and a pyrolysis gas that is flared is also not optimal in terms of energy.
  • a heat-resistant and valve-provided process container is filled with suitably prepared waste in at least one grid-like insert and sealed gas-tight.
  • the preparation of the rubber waste essentially involves the removal of foreign bodies, for example, rims on car tires, or other obviously unsuitable material. If necessary, cleaning may also be required. In the case of car tires in particular, however, it is intended to also shred them.
  • a cutting press in which the press ram is penetrated by cutting edges, has proven itself for shredding.
  • the waste prepared in this way remains in the process container throughout the entire preparation process, which must be designed for the thermal load, since in a second process step the process container with the waste is brought into a process furnace for thermal treatment. During the thermal treatment, the waste is degassed via the valve.
  • a furnace or flame tube is not filled directly with the waste, which then has to be cooled and emptied after degassing. Rather, the degassed waste remains within the process container for the subsequent process steps.
  • this is displayed, for example by sensors, from the process furnace in a cooling chamber, in which the residual heat of the process container with its contents is extracted.
  • the residual heat extracted from the process container is stored in a thermal store and is thus available as process heat that can be reused.
  • the process container and content Once the process container and content have cooled sufficiently, the content can be emptied into a separator for further processing.
  • the gas drawn off during heating via a pipeline connected to the valve is cooled and completely liquefied, temporarily stored in containers for further use.
  • the oil produced by the cooling is a valuable raw material for the chemical industry despite the high sulfur content.
  • the cooling chamber is designed in the manner of a heat exchanger and is provided with a plurality of tubes, that the tubes form at least one circuit for a thermal oil and that the thermal store is provided in the circuit of the thermal oil.
  • the tubes form at least one circuit for a thermal oil and that the thermal store is provided in the circuit of the thermal oil.
  • the process container has a connection for a traction device at the end, that the process container is pulled by the traction device through a first gate into the process furnace, that after degassing the process container from a traction device through one of the first gates Process furnace opposite second gate is pulled into the cooling chamber through an opposite first gate and that after cooling the process container is pulled by a traction device through a second gate opposite the first gate of the cooling chamber.
  • process containers will expediently be provided with rollers or wheels, which may run in or on rails, so that the process container will definitely not break away when pulled.
  • the process container has at least one connection for a hoist or a crane on top, that the process container is lifted into the process furnace by a hoist or a crane, that after degassing the process container is lifted by a hoist or a crane is brought into the cooling chamber through a second gate opposite the first gate of the process furnace, and that after the process container has cooled, the process container is moved by a hoist or a crane through a second gate opposite the first gate of the cooling chamber.
  • a ceiling crane can be envisaged, on the rail (s) of which several trolleys can optionally also be moved.
  • the gates located one behind the other are advantageous because the process takes place inline, so it takes place in one direction and, despite the discontinuous loading, a high throughput can be achieved. This is especially true if there are several Traction devices, hoists or cranes are provided, by means of which the process containers are implemented simultaneously.
  • Another advantage is the provision of a connection arranged opposite a filling opening, at which a hoist or crane can engage in the separating device for emptying the process container.
  • the separator is used to separate the degassed and cooled waste.
  • the separating device has a metal separator and screens of different mesh sizes. The pieces of steel belts in car tires or the like are removed by the metal separator, for example. Sieves of different mesh sizes provide degassed and cooled waste of different, predeterminable sizes.
  • the finest fraction is additionally fed to a ball mill and that the ground material of the ball mill is fed to a roller mill via a sieve.
  • a drum sieve is used as the sieve, so that ultimately finest-grained material with a particle size of 0.1 ⁇ m to 0.5 ⁇ m can be removed from the roller mill.
  • Process container 1 shown in a side view is designed to be movable in a barrel-like manner on wheels or rollers 2.
  • An end face 3 is provided with a gas-tightly closable filling opening for the waste.
  • an eyelet 5 is provided as a connection for a traction means, into which a hook of a chain or a steel cable for pulling or lifting for emptying the process container 1 can be hung through the filling opening .
  • Two further eyelets 6, 7 are provided on the top of the process container 1 for loading the process container 1 with a hoist or a crane.
  • process containers 8 which are provided with grid-like inserts 9, so that there is sufficient space between the individual chunks of material for degassing.
  • the end face 13 also has two eyelets 14, 15.
  • the process containers 1, 8 and 10 are essentially identical in construction and in particular are heat-resistant in order to survive the process explained in more detail below.
  • Figure 4 shows a process container 19 as it is pulled according to arrow 20 by a traction means, not shown further, such as a chain or a steel cable, through an indicated gate 21 in a process furnace 22.
  • a traction means not shown further, such as a chain or a steel cable
  • the waste in the process container 23 located there is degassed at temperatures between 300 ° C. and 500 ° C., depending on the material to be degassed.
  • the process container 23 has a valve, not shown, to which a pipeline 24 is connected. Is cooled and liquefied in a container 25 by a cooling 26 the sulfur-containing oil thus obtained is collected here, for example, in two tanks 27, 28 for later use.
  • a further gate 29 of the process furnace 22 opposite the gate 22 is opened and the process container 23, detached from the pipeline 24, is brought into a cooling chamber 30.
  • the cooling chamber 30 has another gate 31 opposite the gate 29 of the process furnace 22.
  • the process furnace 22 can be continuously heated.
  • the cooling chamber 30 is designed in the manner of a heat exchanger, with a large number of pipes, indicated by the hatching.
  • the pipelines form here, by way of example, three circuits 34 for thermal oil, which are shown in simplified form. Within the three circuits 34, three thermal stores 35-37 are provided, which store the residual heat of the process container 31 at different temperature levels.
  • the thermal accumulator 35 can emit process heat of up to 120 ° C via a heat exchanger 38 for heating purposes in the premises.
  • the second thermal accumulator 36 for temperatures between 120 ° C. and 300 ° C. feeds via a heat exchanger 39, here by way of example, a steam circuit 40 for operating a steam turbine 41 which, coupled with a generator, serves to generate electricity.
  • process heat can again be withdrawn from the steam circuit 40 via a further heat exchanger 42.
  • the two processes explained above can be supported or the heat stored in this thermal accumulator 37 can at least be used for heating the process furnace 22.
  • process container 31 If the process container 31 has cooled sufficiently, it is pulled by a traction device according to arrow 43 in the process container 44 through the gate 33 for emptying.
  • a process container 45 can be transported by means of a crane 46 or another lifting device.
  • trolleys that can be moved on rails 47 are also very suitable for unloading a process container 49, as will be explained below.
  • the process container 49 can be emptied through its filling opening due to gravity into a bunker or the like without any problems or, as in FIG Figure 5 shown in a separating device 51st
  • the separating device 51 has a metal separator 53, which removes metallic foreign bodies such as parts of a steel belt of a car tire.
  • a metal separator 53 which removes metallic foreign bodies such as parts of a steel belt of a car tire.
  • two screens 54, 55 follow the metal separator.
  • the sieve 54 holds back comparatively coarse parts of 3 cm 3 to 4 cm 3 , which are collected in a collecting container 56 for later use.
  • the activated carbon obtained in this way can be processed without hesitation, since it contains no detectable toxins, as gas chromatographic studies have shown.
  • the activated carbon is very clean and of good quality with a very large surface structure.
  • the activated carbon collected in the collecting container 56 can be used, for example, in large filter systems for air treatment as well as in exhaust gas filters, for example in welding systems.
  • the material binds odors effectively and is very absorbent, which means that it can also be used, for example, in printing technology with biological inks to bind the very strong odors.
  • Chunks with a size of 1 cm 3 to 2 cm 3 are sieved out through the second sieve 55 and fed to a further collecting container 57.
  • This finer material is ideally suited for use in relatively small air treatment filters, for example in large offices, waiting rooms of medical practices or the like. Physical vapors are also perfectly bound by the material.
  • a drum screen 59 is also indicated schematically, which is permeable, for example, to a finely ground powder with a grain size of 5 ⁇ m and returns larger particles to the ball mill 58.
  • a powder with a particle size of 10 ⁇ m can be used as a filler in the manufacture of plastics.
  • a powder with a grain size of less than 5 ⁇ m can be used again in rubber production. Kneaded into a raw rubber mass, this material serves the same purpose as carbon black and also has better absorbency.
  • a fine powder can also be used as a pigment in the paint industry. If necessary, the fine material from the roller mill 60 can also be ground more finely in a wet mill.

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  • Chemical & Material Sciences (AREA)
  • Engineering & Computer Science (AREA)
  • Oil, Petroleum & Natural Gas (AREA)
  • Organic Chemistry (AREA)
  • Materials Engineering (AREA)
  • Combustion & Propulsion (AREA)
  • Environmental & Geological Engineering (AREA)
  • Life Sciences & Earth Sciences (AREA)
  • Mechanical Engineering (AREA)
  • Wood Science & Technology (AREA)
  • Chemical Kinetics & Catalysis (AREA)
  • General Chemical & Material Sciences (AREA)
  • Physics & Mathematics (AREA)
  • Thermal Sciences (AREA)
  • Processing Of Solid Wastes (AREA)
  • Separation, Recovery Or Treatment Of Waste Materials Containing Plastics (AREA)
  • Processing And Handling Of Plastics And Other Materials For Molding In General (AREA)

Claims (7)

  1. Procédé, destiné à la préparation de déchets polymères et/ou organiques, lequel comporte les étapes suivantes, consistant :
    - en ce qu'on remplit un conteneur d'opération (8, 23) résistant à la chaleur et muni d'une soupape de déchets préparés en conséquence dans au moins un insert (9) grillagé et on le ferme de manière étanche aux gaz,
    - en ce qu'on amène le conteneur d'opération (8, 23) contenant les déchets pour un traitement thermique dans un four de processus (22), en ce que pendant le traitement thermique, il s'effectue un dégazage via la soupape et en ce que par l'intermédiaire d'une tuyauterie (24) raccordée sur la soupape, on soutire le gaz, qui refroidi et liquéfié est entreposé dans des citernes (27,28) pour une utilisation ultérieure,
    - en ce que directement après le dégazage, on transfère le conteneur d'opération chauffé du four de processus (22) dans une chambre de refroidissement (30), dans laquelle la chaleur résiduelle est soutirée du conteneur d'opération (32), et en ce que la chaleur résiduelle est stockée dans un accumulateur thermique (35 à 37) en tant que chaleur de processus réutilisable, et
    - en ce qu'une fois le refroidissement effectué, on retire le conteneur d'opération de la chambre de refroidissement (30) et en ce qu'on vide le contenu du conteneur d'opération (49) dans un dispositif séparateur (51) en ce que
    - sur un raccord (50) placé au vis-à-vis d'un orifice de remplissage s'engage un engin de levage ou une grue (48) pour soulever et vider par la suite le conteneur d'opération (49).
  2. Procédé selon l'une quelconque ou plusieurs des revendications précédentes, caractérisé en ce que la chambre de refroidissement (30) est conçue à la manière d'un échangeur thermique, pourvu d'une pluralité de tubes, en ce que les tubes forment au moins un circuit (34) pour une huile thermique et en ce que dans le circuit de l'huile thermique est prévu l'accumulateur thermique (35 à 37).
  3. Procédé selon la revendication 2, caractérisé en ce que de la chaleur de processus est soutirée de l'au moins un accumulateur thermique (35 à 37).
  4. Procédé selon l'une quelconque ou plusieurs des revendications précédentes, caractérisé en ce que le conteneur d'opération (8,23) comporte en face frontale un raccord (5) pour un moyen de traction, en ce que le conteneur d'opération (19), tiré par un moyen de traction est amené à travers un premier portail (21) dans le four de processus (22), en ce qu'après le dégazage, le conteneur d'opération (23) est tiré par un moyen de traction à travers un deuxième portail (29) opposé au premier portail (21) du four de processus (22) à travers un premier portail (31) opposé dans la chambre de refroidissement (30) et en ce qu'après le refroidissement, le conteneur d'opération (32) est tiré par un moyen de traction à travers un deuxième portail (33) opposé au premier portail (31) de la chambre de refroidissement (30).
  5. Procédé selon l'une quelconque ou plusieurs des revendications précédentes 1 à 3, caractérisé en ce que le conteneur d'opération comporte en face supérieure au moins un raccord pour un engin de levage ou une grue, en ce que le conteneur d'opération, soulevé par un engin de levage ou une grue est amené à travers un premier portail dans le four de processus, en ce qu'après le dégazage, le conteneur d'opération est amené par un engin de levage ou une grue à travers un deuxième portail opposé au premier portail du four de processus à travers un premier portail opposé dans la chambre de refroidissement et en ce qu'après le refroidissement, le conteneur d'opération est amené par un engin de levage ou une grue à travers un deuxième portail opposé au premier portail de la chambre de refroidissement.
  6. Procédé selon l'une quelconque ou plusieurs des revendications précédentes, caractérisé en ce que le four de processus (23) et/ou la chambre de refroidissement (30) fonctionne(nt) en continu.
  7. Procédé selon l'une quelconque ou plusieurs des revendications précédentes, caractérisé en ce que le dispositif séparateur (51) comporte un séparateur de métaux (53) et des tamis (54, 55) de différent maillage, en ce que la fraction la plus fine est alimentée vers un broyeur à billes (58) et en ce que le produit broyé du broyeur à billes (58) est alimenté par l'intermédiaire d'un tamis (59) vers un moulin à cylindres (60).
EP15750623.9A 2014-05-26 2015-05-26 Méthode de traitement de déchets polymères Active EP3149111B1 (fr)

Priority Applications (1)

Application Number Priority Date Filing Date Title
PL15750623T PL3149111T3 (pl) 2014-05-26 2015-05-26 Sposób przetwarzania odpadów polimerowych

Applications Claiming Priority (2)

Application Number Priority Date Filing Date Title
DE102014007595.8A DE102014007595A1 (de) 2014-05-26 2014-05-26 Verfahren der Aufbereitung von polymeren Abfällen
PCT/DE2015/000257 WO2015180704A1 (fr) 2014-05-26 2015-05-26 Procédé pour le traitement de déchets polymères

Publications (2)

Publication Number Publication Date
EP3149111A1 EP3149111A1 (fr) 2017-04-05
EP3149111B1 true EP3149111B1 (fr) 2020-07-08

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Country Status (9)

Country Link
US (1) US10465122B2 (fr)
EP (1) EP3149111B1 (fr)
JP (1) JP6714583B2 (fr)
CA (1) CA2949180A1 (fr)
DE (2) DE102014007595A1 (fr)
EA (1) EA032653B1 (fr)
ES (1) ES2820767T3 (fr)
PL (1) PL3149111T3 (fr)
WO (1) WO2015180704A1 (fr)

Families Citing this family (3)

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Publication number Priority date Publication date Assignee Title
DE102016208602B4 (de) * 2016-05-19 2021-10-14 Volkswagen Aktiengesellschaft Thermoplastischer Kunststoff mit Pyrolysekohle als Füllstoff, Kunststoffteil für die Innenausstattung eines Fahrzeuges sowie Verwendung von Pyrolysekohle in Schmelzen von thermoplastischen Kunststoffen
US20190359891A1 (en) * 2018-05-25 2019-11-28 Plus5, Inc. Pyrolysis system for solvents, carbon and other pyro-products
TWI806810B (zh) * 2023-01-05 2023-06-21 能創科技股份有限公司 熱裂解系統

Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050234274A1 (en) * 2002-04-26 2005-10-20 Bernd Peggy D Method and installation for low-temperature pyrolysis of rubber products, steel/rubber composites, and use of the pyrolysis products

Family Cites Families (19)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US3068812A (en) * 1959-05-07 1962-12-18 Wesley C L Hemeon Method and apparatus for incinerating combustible wastes
DE2826918A1 (de) 1978-06-20 1980-01-10 Babcock Ag Verfahren zur verwertung von gummi- und kunststoffabfaellen, insbesondere von altreifen
US4401513A (en) * 1980-09-26 1983-08-30 Brewer John C Apparatus for pyrolyzing shredded tires
FR2745819B1 (fr) * 1996-03-11 1999-04-09 Seit Installation de traitement thermique de dechets industriels, hospitaliers, menagers et assimilables avec protection de l'environnement au-dela des normes fixees
HU1448U (en) 1997-10-06 1998-12-28 Barsi Continuous closed pyrolysis system for treating of waste rubber
ES2166945T3 (es) 1997-12-22 2002-05-01 Alcyon S A Procedimiento para el tratamiento de caucho y plasticos usados.
DE10150696A1 (de) 2001-10-17 2003-05-08 Dieter Brunsendorf Verfahren und Vorrichtung zur thermischen Verwertung von Altgummiprodukten
JP3623204B2 (ja) * 2002-03-22 2005-02-23 越智 洋太郎 乾溜熱分解システム
DE10348987B4 (de) 2003-10-17 2006-01-12 Merenas Establishment Vorrichtung zur Durchführung einer Niedrigtemperaturpyrolyse von Gummierzeugnissen und -Verbundprodukten
PL364607A1 (en) * 2004-01-27 2005-08-08 Ingo Schramm Method and system for treating organic waste, particularly rubber containing waste
DE102005038827B4 (de) 2005-08-17 2010-02-11 Chi-Hsiang Wang Verfahren zur Herstellung eines künstlichen Kohleadsorptionsmittels aus Bambus
JP4362727B2 (ja) * 2005-08-31 2009-11-11 株式会社オールマイティー 油化装置及び油化装置の残渣排出方法
DE202007014636U1 (de) * 2007-10-19 2008-01-10 Karl Ley Gmbh Industrieofenbau Pyrolysevorrichtung
DE102008010758A1 (de) * 2008-02-23 2009-09-10 SWU Gesellschaft für Umwelttechnik mbH Verfahren zur Pyrolyse von organischen Abfallstoffen und Biomaterialien
JP2010013329A (ja) * 2008-07-04 2010-01-21 Haruo Shiraishi 高分子廃棄物からの活性炭製造システム
WO2010012275A2 (fr) 2008-07-28 2010-02-04 Corina Projahn Produit de pyrolyse et son utilisation
JP2010138333A (ja) * 2008-12-15 2010-06-24 Masayuki Tsutsui 廃タイヤ油化装置
CN103351883B (zh) * 2013-06-08 2014-11-19 中国科学院地球化学研究所 一种生物质碳化工艺和设备
CZ26384U1 (en) * 2013-09-04 2014-01-28 Hedviga Group A.S. Apparatus for producing fuels for energy use

Patent Citations (1)

* Cited by examiner, † Cited by third party
Publication number Priority date Publication date Assignee Title
US20050234274A1 (en) * 2002-04-26 2005-10-20 Bernd Peggy D Method and installation for low-temperature pyrolysis of rubber products, steel/rubber composites, and use of the pyrolysis products

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ES2820767T3 (es) 2021-04-22
JP6714583B2 (ja) 2020-06-24
CA2949180A1 (fr) 2015-12-03
JP2017519891A (ja) 2017-07-20
US20170073583A1 (en) 2017-03-16
EA032653B1 (ru) 2019-06-28
EA201692387A1 (ru) 2017-05-31
DE102014007595A1 (de) 2015-11-26
WO2015180704A1 (fr) 2015-12-03
US10465122B2 (en) 2019-11-05
PL3149111T3 (pl) 2021-02-08
EP3149111A1 (fr) 2017-04-05

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